[0001] - Process and apparatus for dissociating the hydrogen atoms of a water molecule by
electrical force. Particularly, the separation of the hydrogen and oxygen atoms from
the water molecule by the application of a non-regulated, non-filtered, low-power,
direct current voltage electrical potential applied to two non-oxidizing similar metal
plates having water passing therebetween. The direct current.voltage may be continuous,
but the sub-atomic action is enchanced by pulsing the non-regulated and non-filtered
direct current voltage.. The apparatus comprises constructional configurations and
there is disclosed alternative embodiments for segregating the generated hydrogen
gas from the oxygen gas. The water need not be pure and may contain contaminents.
The release of the hydrogen and oxygen atoms causes the contaminents to fall away,
thereby enabling the system to be utilized in a liquid slurry removal system. Alternatively,
the recombining of the hydrogen and oxygen would give pure water.
BACKGROUND
[0002] The potential availability of hydrogen as a supplement to and eventually completely
replace the present day available fuels is most appreciated. The efficiency of hydrogen
as a fuel and its pollution free qualifies further enchances its attractiveness.
[0003] The prior art systems have been successful in splitting the hydrogen atoms from the
oxygen. However, costs_per Btu is most prohibitive and completely restricts the known
process from commercialization.
[0004] The most commonly understood method of separating the hydrogen and oxygen atoms from
water is electrolysis. This comprises placing a direct current voltage in a solution
of water and potasium hydroxide, When current flows, an exchange of ions and electrons
occurs between the electrodes. Hydrogen atoms collect at the negative electrode (cathode)
and oxygen atoms at the positive electrode (anode). A separation between the electrodes
separates the gases.
[0005] Significantly this process requires a chemical solution; that is, it does not process
the hydrogen from pure water. Furthermore, the cost per million Btu is in the order
of three times the cost of gasoline.
[0006] Other electrolysis processes have been devised and di
s- closed; but, again the more sophisticated, the complicated, complex and costly with
the attendant unreliability.
[0007] Another process under study comprises nuclear energy to supply heat in a thermal
of the hydrogen dissociation. The problems with the process include the lack of container
materials that can withstand temperatures of(3,700 degrees F) and a practical method
of attaining such temperatures. The addition of inorganic compounds to the water permits
lower temperatures but again, adds to the complexity of the process.
[0008] A commercial method known as the Bosch process, consists in passing steam over highly
heated carbon in the presence of a suitable catalyst. Carbon monoxide, CO, and hydrogen
are first formed as shown in the following equation:

[0009] The resulting carbon monoxide then reacts with more steam, forming carbon dioxide
and hydrogen:

[0010] The carbon dioxide is separated from the hydrogen by passing the mixture through
water under pressure; the carbon dioxide dissolves in the water and leaves the hydrogen
pure or nearly so..
[0011] Another process consists in the action of steam on methane, CH
4. The equations for the reactions that take place are:

[0012] The resulting carbon dioxide and hydrogen are separated as in Bosch process. In a
similar way, hydrogen may be obtained from other hydrocarbons.
[0013] Hydrogen is also obtained as a by-product from processes designed to prepare other
substances, for example, in the preparation of chlorine by electrolysis of sodium
chloride solution:

[0014] H
2 + Cl
2 and other important processes. The symbol (aq) tells us that the substances are present
in water (aqueos) solutions.
[0015] Finally, there is the nature way of attaining hydrogen by photosynthesis. At best
the process is still in the laboratory small-scale stage and those in the art acknowledges
the process can produce hydrogen with an efficiency of only 37%.
[0016] It is generally understood among scientists that all forms of hydrogen production
must be explored -- even if it is too costly, inefficient, or impractical. But, more
significantly, hydrogen will be the fuel of the future. The only question remains
how and when it will be produced.
[0017] Reference is made to the publication Cheaper Hydrogen. Popular Science, September
1981, pages 10 through 14, that reviews and updates the above-noted processes for
disassociating the hydrogen atom.
SUMMARY OF INVENTION
[0018] The process of the present invention, unlike those of the prior art, is a simple,
efficient, and low cost process for separating the hydrogen and oxygen atoms from
water. No chemicals are added to the water and the electrical power utilized is only
negligible.
[0019] In its most fundamental concept the water (may be pure, salt water, or contaminated
water) is passed between two plates of similar non-oxidizing metal. The one plate
has placed thereon a positive potential and the other a negative potential from a
very low direct voltage current power source. The hydrogen atoms are separated and
collected for utilization.
[0020] The contaminants in the water is forced also to dissociate itself and may be collected
or utilized and disposed of. This in turn lends the process to recombining the hydrogen
and oxygen into pure water.
[0021] The direct current voltage is non-regulated and non-filtered. Experimentation demonstrated
that the direct current voltage acts as a static force on the water molecules; whereas
the rippling direct current voltage acts as a dynamic force. Pulsating the direct
current further acts as a dynamic force and enhances considerably the splitting of
the atoms from the water molecules.
[0022] The apparatus for carrying out the process is extremely simple and can be manufactured
most inexpensively. Certain plate arrangements and configurations are disclosed with
graphical illustration of relative efficiency. Alternative structure for separating
and collecting the hydrogen from the oxygen is disclosed.
OBJECTS
[0023] It is accordingly a principal object of the present invention to provide method and
means for a hydrogen/oxygen generator that is operable from any natural water source
irrespective of its purity.
[0024] Another object of the present invention is to provide such a hydrogen/oxygen generator
that is operable from every low electrical power, extremely efficient, and wherein
the cost of operation ia most minimal.
[0025] Another object'of the present invention is to provide a hydrogen/oxygen generator
from water containing contaminents, and thereafter recombining the hydrogen/oxygen
to form pure water.
[0026] Still another object of the present invention is to provide a hydrogen/oxygen generator
that utilized apparatus of simple and low cost materials, and which structure can
be made in varying sizes, and duplicated without loss of efficiency.
[0027] Other objects and features of the present invention will become apparent from a reading
of the detailed description of the preferred embodiment and it-s alternative structures
when taken in conjunction with the drawings in which
BRIEF DESCRIPTION OF DRAWINGS
[0028]
Figure 1 is an illustration in cross-section of the operable constructed preferred
embodiment of the present invention.
Figure 2 illustrates the coaxial cluster or array of plates utilized in the embodiment
of Figure 1.
Figure 3 is a first alternative plate arrangement, a concentric coaxial array.
Figure 4 is another alternative plate arrangement, the flat plate array.
Figure 5 illustrates the voltage potential as applied to several plates.
Figure 6 illustrates the principles of the present invention in its most simplified
embodiment.
Figure 7 is theppreferred embodiment shown in Figure 1 except in this illustration,
the view is perspective.
Figure 8 is a graphical illustration of applied power versus gas generated, and effect
as to . condition of water.
Figure 9 is a graphical illustration of applied power versus gas generated, and increases
in water temperatures.
Figure 10 is a graphical illustration of gas generator versus tube length in a tubular
plate arrangement.
Figure 11 is a graphical illustration of applied.power versus gas generated for pure
water.
Figure 12 is a graphical illustration of gas generation for three different geometrical
configurations of plate structure.
Figure 13 is a graphical illustration of gas generated with the plates having increasing
separation, and
Figure 14 is a graphical illustration of electrical costs versus gas generated, and
increases in Exciter Plate 5.
Figure 15 is a graphical illustration of different-applied power versus gas generated,
for various types of water conditions.
Figure 16 is a gas generated versus pulse direct current repitition rate.
DETAILED DESCRIPTION OF INVENTION AS DEPICTED IN DRAWINGS
[0029] With particular reference now to figure 6, there is illustrated schematically in
cross-section the invention in its most simplified embodiment.
[0030] A structure 110 contains a water supply 15 comprising molecules 62a xxx 62n, of hydrogen
38a xxx 38n, oxygen, 39a xxx 39n, and foreign substances 64a xxx 64n. A pair of plates
9a and 9n consisting of non-oxydizing metal -- and both of the same metal, are submerged
in the water 15.
[0031] Attached to terminal 32 on the first of the plates 9a is a wire having its other
end connected to the negative terminal there is connected another wire having its
other end connected to the positive terminal of the aforesaid direct current voltage
electrical source 30.
[0032] The direct current voltage applied to the water passing between plates 9a and 9b
is sufficient to dissociate the hydrogen atom 39a x x x 39n and oxygen atoms 38a x
x x 39n (appearing as bubbles) from the water molecules 62a xxx 62n. The forceful
action of the applied potential attacks the molecule structure of the water and not
its atomic structure, i.e., sub-atomic.
[0033] The foreign substance or contaminents 64a xxx 64n is broken away from the water molecule
62a xxx 62n, and spills over the outside area of the plates 9a and 9b to a collector
at the bottom of the tank 110.
[0034] The hydrogen gas 63a xxx 63n and oxygen gas 65a xxx 65n rises above the liquid. The
gasses are separated, collected and thereafter utilized all as set forth below.
[0035] The process shown with the apparatus of Figure 6 is operable, as depicted schematically,
in its most crude form. To increase and enchance the action, the process and the apparatus
is improved upon as shown in the constructed and preferred embodiment of Figure 1
in cross-section and Figure 10 in perspective.
[0036] The voltage source 30 (shown schematically in Figure 5) supplies a direct current
voltage that is rectified bur-not filtered and not regulated. That is, the direct
current voltage is rippled and unregulated. The varying amplitude peeks., ripples,
in terms of applied force acts as a constant static physical force.
[0037] The amount of electrical power required by the hydrogen/ oxygen generator of the
preferred embodiment, as illustrated, is surprisingly minimal. For the embodiment
shown in Figures 2 and 10, the source 30 supplied 12 volts at 1 ampere to terminal
4.
[0038] It can be appreciated, that increasing the voltage would enhance the forceful sub-atomic
action upon the water molecule. With reference to Figure 11, the voltage current versus
gas generated is illustrated graphically. The gas generated is a linear function to
magnitude of voltage applied. However, there is a serious limitation to increasing
the voltage. As.the voltage/ current is increased the. temperature of the water increases
and eventually reaches a condition where steam is generated -- as illustrated graphically
in Figure 10 Further as;shown graphically in Figure 9 the current versus gas generated
is also a function of the type of water utilized.
[0039] Therefore, in lieu of increasing the electrical power to enchance the sub-atomic
action on the water molecules, other conditions have been considered. The first is
to alter the plate source direct current.voltage waveform.
[0040] With particular reference to Figure 5 there is illustrated an electronic switch for
switching on and off the rippled d.c output of supply 30. The ripple is not removed.
The plates 32a x x x 32n are connected to a common ground 34. The positive terminals
33a x x x 33n are connected respectively to contacts 31a x x x 31n of switch 35 rotatively
making and breaking contact with the direct-current voltage source 30.
[0041] In function the pulsed rippled output voltage forcefully applies to the water molecules
a dynamic force, the pulse repitition rate versus the gas generated.
[0042] Other structured factors altering, affecting, and particularly enhancing the hydrogen
gas generating comprises altering (1) plate size, (2) plate spacing, (3) number of
plates, and (4) the plate configuration. Each of these factors have been taken into
consideration in the development of a plate configuration to provide optimum results
for a preferred embodiment.
[0043] With reference to Figure 2, there is shown an array or cluster of tubular plates
utilized in the preferred embodiment of Figures 1 and 7 The term "plate" hereinafter,
is intended to convey a large area electrical surface; and whether the surface is
flat, curved, tubular or otherwise, is of no consequence except as hereinafter defined.
Particularly each tubular plate-comprises an outside tube 32a x x x 32n, and an inside
tube 33a x x x 33n. Connecting each of the center tubes 33a x x x 33n is a terminal
wire 34; and connecting each of the outside tubes the through a common ground is a
terminal wire-36. The two terminal wire 34 and 36 are connected to the positive and
negative side respectively of the direct current voltage source 30. Intermediate the
outside and inside tubes are a series of spacers 35a x x'x 35n. The coaxial tubes
in an array are shown pictorially in the perspective view of Figure 7 .
[0044] With particular reference to Figure 3 there is illustrated, as an alternative to
that utilized in the preferred embodiment, another plate arrangement and configuration.
This concentric ring array comprises a series of tubes each being co-axial with the
other and of a size equally larger than its inner adjacent tube. The center tube 38a
and the alternate tubes 38b and 38c serve as the positive plates connected to positive
wire terminal 36. Each of the tubular plates 38a, 38b, and 38c are interconnected
via connectors 8a and 8d to wire terminal 34. The three spacers .39a, 39b, and 39c
maintain a uniform spacing between the respective tubular plates.
[0045] With particular reference to Figure 4 there is shown still another plate arrangement
and configuration. In this embodiment, shown in cross-section, the positive plates
9a x x x 9n are interconnected by electrode 12a whereas the negative plates lla x
x x lln are interconnected by the electrode 12b.
[0046] With particular reference to 12 there is illustrated graphically the efficiency of
the tubular plate array of Figure 2, the cluster tubular array of Figure 3, and the
flat plate array of Figure 4. Specifically there is shown the gas generation versus
the plate configuration. It can be appreciated from this graph why the embodiment
of Figure 1 includes.the cluster tubular array of Figure 2.
[0047] As stated above another factor affecting the gas generation output is the plate separation.
With particular reference to Figure 13 there is illustrated graphically plate spacing
versus gas generation. As can be seen the greater the spacing the les.s gas generation.
The efficiency versus spacing of the plates is a linear decrease with spacing.
[0048] As stated above the applied direct current voltage across' the positive current voltage
plates having water therebetween is a force applied -- in the.nature of a physical
force -- to the water molecules. The applied force is sufficient-to cause the hydrogen
and oxygen atoms to dissociate themselves from the water molecule and anything else
that may be included therewith.
[0049] In the aforementioned prior art system of hydrogen gas generation such as the electrolysis
process., it is essential that the'water be distilled or otherwise made pure.
[0050] To determine the relative differences of the amount of gas generated versus the purity
of the water, analysis was made of distilled water, rain water, city tap water, river
water, well water untreated, well water treated, and sea water. The results of gas
generation versus electrical power is illustrated in Figures- 8 and 15 graphically
for each of the waters tested.
[0051] It appears that water containing contaminents.aids gas generation; however, the nature
of the water contaminents appears to have no.significance. The hydrogen atoms and
oxygen atoms dissociate themselves from the water molecule. Anything else that may
be included in the water is also bombarded loose and overflows the tank 37 and falls
to the bottom 43.
[0052] Having now examined the applied electrical force phenomena, the physical configuration
of the electrical plates, the power applied, and the condition of the water, reference
is made specificially to the constructed function and operation constructed and operable
preferred embodiment of the hydrogen gas generator of the present invention shown
in cross-section in Figure 1 and in perspective in Figure 7.
[0053] The container 10 is a square elongated box configuration completely enclosing and
sealing the components.as hereinafter described.
[0054] Water, from which the hydrogen gas is to be taken, enters via inlet 42 to the chamber
36. The water is pumped or enters under normal pressure from a source via line 56.
As mentioned above, the water need not be pure and hence may originate from any source.
The water from source 42 enters chamber 36 which is a free area to an open top enclosure
37.
[0055] The water entering chamber 36 is caused to rise upwardly through the plates of the
Cluster.60 previously described in more detail relative to Figure 2.
[0056] Applied to the inner tubular structures is a positive direct current voltage, and
to the outer tubular structures of the cluster array 60 is applied a negative direct
current voltage. The direct current voltage is applied via terminals 4 connected to
a suitable direct current voltage power source 30.
[0057] The hydrogen gas is depicted in Figure 1 as a solid circle 38, whereas the oxygen
gas is depicted as the open circles 39.
[0058] The separated hydrogen and oxygen gas rises into the accumulator chamber 47.
[0059] Not all of the water molecules is broken up into its various atomic components. Thus,
the unspent water 41 spills over the top of chamber 37 and drops down through outer
chamber 54 and back to reservoir 43.
[0060] As aforesaid, it is not necessary to utilize pure water, the intake water will include
several forms of contaminents. As best understood, when the water molecule-is bombarded
with the dynamic and static electrical force, the contaminents adhering to the water
molecules are shaken loose and released therefrom. The contaminents, too, rise to
the top of chamber 37 and form a part of the spillway 41. In that the containments
do not contain hydrogen or oxygen, there will be no atomic breakup. The combination
of water with contaminents drops down into ex- traction chamber 43.
[0061] In the extraction chamber 43 most of the sediment or sludge will drop to the bottom
of the chamber 32. The water with most of the sediment removed passes through the
ports 33a xxx 33n, through charcoal filter 31, and into return water chamber 44. The
uppermost portion of the water in chamber 44 drops into standpipe 35.
[0062] The water cleansed of substantially all contaminents exits via pipe 45 and then through
line 55 and back to inlet pipe 42. The combined water from inlets 55 and 56 is again
processed as aforesaid.
1. A system for the non-ionic release of hydrogen gas and oxygen gas from natural
water, characterized by a non oxydizing housing having a reservoir for retaining natural
non-electrolytic water therein, a pair of similar non-oxydizing plates positioned
in said water, a direct voltage/current source including means for connecting one
of said plates to the negative terminal and the other of said plates to the positive
terminal of said source, said direct voltage/current potential on said plates causes
a sub-atomic force-type action on said water, thereby disassociating the hydrogen
atoms and oxygen atoms from the water molecules.
2. The systen as set forth in claim 1, characterised in that said voltage/current
potential is an unfiltered and non-regulated voltage and/or is pulsed.
3. The system as set forth in claim 2, characterized in that said pulsed direct voltage/current
potential includes means to control the repetition rate thereof.
4. The system as set forth in claim 1, characterized in that said direct voltage/current
potential includes means for varying the amplitude of said potential.
5. The system as set forth in claim 1, characterised in that said natural water contains
contaminents and that said contaminents are released by said sub-at-omic force on
the water molecules, and means for collecting said contaminents.
6. The system as set forth in claim 1, characterized in that said non-oxydizing plates
have a flat. or alternatively a nonplanar surface.
7. The system as set forth in claim 1, characterized in that'said non-oxydizing plates
are coaxial or alternatively have a-concentric surface.
8. The system as set forth in claim 1, characterized in that said non-oxydizing plates
are a plurality of plates in an array.
9. The system as set forth inclaim 1, characterized in-that said non-oxydizing plates
are a cluster of coaxial plates in an array.
10. The system as set forth in claim 1, characterized in that said positive and negative
non-oxydizing plates are varied in spacing and/or in length and/or in surface area.
11. The system as set forth in claim 1, characterized in that said non-oxydizing housing
further comprises a gas collection chamber for maintaining a preset volume of gas
under pressure.
12. The system as.set forth in claim 1, characterized in that the configuratinn of
said plates is directly related to the forceful action of said direct current voltage
potential on said water molecules.
13. The system as set forth in claim 8, characterized by switching means interconnected
to each of said plates in said array and to said voltage source for switching in and
out selected ones of said array of plates from said voltage source.
14. The process of non-ionic releasing hydrogen and oxygen gas from non-electrolytic
water, characterized by passing said non-electrolytic water through a contained area
having a pair of non-oxydizing electrically conductive plates therein, applying a
direct current electric positive potential across one of said plates and applying
a direct current electric negative potential across the other of said plates, said
electrical power potential applied to said plates being of sufficient magnitude to
cause the positive atoms of the water molecule to be attracted to the negative potential
on said plate and the negative atoms of the water molecule to be attracted to the
positive potential on said plate, thereby forcing the hydrogen atoms and the oxygen
atoms to disassociate themselves from the water molecule.